WO2001029153A1 - Procede de modification de carburant hydrocarbone et dispositifs de modification de carburant hydrocarbone - Google Patents

Procede de modification de carburant hydrocarbone et dispositifs de modification de carburant hydrocarbone Download PDF

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Publication number
WO2001029153A1
WO2001029153A1 PCT/RU2000/000380 RU0000380W WO0129153A1 WO 2001029153 A1 WO2001029153 A1 WO 2001029153A1 RU 0000380 W RU0000380 W RU 0000380W WO 0129153 A1 WO0129153 A1 WO 0129153A1
Authority
WO
WIPO (PCT)
Prior art keywords
mixture
fuel
fact
τοπliva
source
Prior art date
Application number
PCT/RU2000/000380
Other languages
English (en)
Russian (ru)
Inventor
Leonid Yakovlevich Gandelman
Andrei Grigorievich Lyapin
Original Assignee
Leonid Yakovlevich Gandelman
Andrei Grigorievich Lyapin
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Leonid Yakovlevich Gandelman, Andrei Grigorievich Lyapin filed Critical Leonid Yakovlevich Gandelman
Priority to CA002386612A priority Critical patent/CA2386612A1/fr
Priority to JP2001531940A priority patent/JP2003512503A/ja
Priority to EA200200464A priority patent/EA003680B1/ru
Priority to AU75643/00A priority patent/AU7564300A/en
Priority to US10/110,875 priority patent/US6692634B1/en
Priority to KR1020027004898A priority patent/KR20020052189A/ko
Priority to EP00964818A priority patent/EP1241243A4/fr
Publication of WO2001029153A1 publication Critical patent/WO2001029153A1/fr

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G27/00—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation
    • C10G27/04—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation with oxygen or compounds generating oxygen
    • C10G27/14—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation with oxygen or compounds generating oxygen with ozone-containing gases

Definitions

  • the invention is subject to chemistry, in particular to the technology of hydrocarbon fuels and may be used in various ways.
  • SIGNIFICANT FOX Heavier carbohydrates in lighter fractions, which also cause significant, often up to 50-60%, of the general initial volume of fuel.
  • P ⁇ s ⁇ avlennaya task ⁇ eshae ⁇ sya ⁇ em, ch ⁇ in s ⁇ s ⁇ be m ⁇ di ⁇ i ⁇ atsii uglev ⁇ d ⁇ dn ⁇ g ⁇ ⁇ liva ⁇ dachu ⁇ liva ⁇ ⁇ susches ⁇ vlyayu ⁇ ezhe ⁇ tsiey in ⁇ chnuyu ⁇ ame ⁇ u and z ⁇ nu ezhe ⁇ tsii ⁇ dayu ⁇ ⁇ z ⁇ n ⁇ s ⁇ de ⁇ zhaschy gas, ⁇ b ⁇ az ⁇ vann ⁇ y dvu ⁇ azn ⁇ y mixture s ⁇ zdayu ⁇ ⁇ u ⁇ bulen ⁇ nye ⁇ i and ⁇ e ⁇ b ⁇ az ⁇ vannuyu mixture na ⁇ avlyayu ⁇ in ⁇ bem s ⁇ s ⁇ abilnym pressure u ⁇ vnem and ⁇ v ⁇ dya ⁇ ⁇ e ⁇ m ⁇ dinamiches ⁇ e
  • Task 25 ⁇ eshae ⁇ sya ⁇ a ⁇ zhe ⁇ em, ch ⁇ ⁇ e ⁇ ed ⁇ b ⁇ az ⁇ vaniem ⁇ u ⁇ bulen ⁇ ny ⁇ ⁇ v s ⁇ zdayu ⁇ uchas ⁇ on ⁇ m ⁇ dvu ⁇ azn ⁇ y mixture za ⁇ uchivayu ⁇ v ⁇ ug ⁇ si ⁇ chn ⁇ y ⁇ ame ⁇ y and ezhe ⁇ tsiyu is ⁇ dn ⁇ g ⁇ ⁇ liva in ⁇ chnuyu ⁇ ame ⁇ u ⁇ susches ⁇ vlyayu ⁇ s ⁇ offset ⁇ n ⁇ si ⁇ eln ⁇ its ⁇ si.
  • Task 30 ⁇ eshae ⁇ sya ⁇ a ⁇ zhe ⁇ em, ch ⁇ ⁇ e ⁇ b ⁇ az ⁇ vannuyu mixture ⁇ il ⁇ uyu ⁇ ⁇ ⁇ eny, ⁇ ve ⁇ dy ⁇ v ⁇ lyucheny and v ⁇ dny ⁇ ⁇ as ⁇ v ⁇ v gid ⁇ isl ⁇ v ⁇ imesey ⁇ liva and g ⁇ vy ⁇ du ⁇ na ⁇ avlyayu ⁇ on v ⁇ d ⁇ chn ⁇ y ⁇ ame ⁇ y and ⁇ tsess ⁇ v ⁇ yayu ⁇ ⁇ at me ⁇ e still ⁇ din ⁇ az.
  • Task 35 also ⁇ eshae ⁇ sya ⁇ em, ch ⁇ in ⁇ tsesse ⁇ e ⁇ m ⁇ dinamiches ⁇ g ⁇ vy ⁇ avnivaniya ⁇ a ⁇ ame ⁇ v in dvu ⁇ aznuyu mixture ⁇ dayu ⁇ ⁇ as ⁇ ylennuyu v ⁇ du and ⁇ luchennuyu emulsion ⁇ dve ⁇ gayu ⁇ ⁇ e ⁇ m ⁇ dinamiches ⁇ mu vy ⁇ avnivaniyu ⁇ a ⁇ ame ⁇ v and ⁇ v ⁇ dya ⁇ gid ⁇ i ⁇ vanie and v ⁇ ss ⁇ an ⁇ vlenie with ⁇ sleduyuschim
  • Emulsions on the fractions of hydrocarbons and filters, steam and cleaned and enriched part of them are directed to the input of the camera and the process is less necessary.
  • the emulsion is electrically hydraulically separated, and after the inactive part of the mixture is inactive, the process is inactive.
  • the task is solved by the creation of a device for modifying
  • the task is also solved in order that the device for enrichment and processing of the original fuel is carried out with a filter on
  • the process converter is designed as a simple camera with power switches that are disconnected from the source of electric pulses and emulsions
  • At least one simple cylindrical camera and / or diffuser are equipped with electromagnet filters.
  • the task is also solved by the creation of a device for modifying hydrocarbon fuel containing a source of output
  • 25 and ⁇ b ⁇ gascheniya ⁇ e ⁇ b ⁇ az ⁇ vaniya is ⁇ dn ⁇ g ⁇ ⁇ liva, vy ⁇ lnenn ⁇ mu of ⁇ sled ⁇ va ⁇ eln ⁇ s ⁇ edinenny ⁇ dvu ⁇ ⁇ chny ⁇ tsilind ⁇ iches ⁇ i ⁇ ⁇ ame ⁇ between ⁇ ymi ⁇ azmeschen ele ⁇ gid ⁇ dinamiches ⁇ y ⁇ e ⁇ b ⁇ az ⁇ va ⁇ el ⁇ a and ⁇ at me ⁇ e of dvu ⁇ ⁇ ame ⁇ ⁇ e ⁇ m ⁇ dinamiches ⁇ g ⁇ vy ⁇ avnivaniya
  • Task 35 ⁇ eshae ⁇ sya ⁇ a ⁇ zhe and ⁇ em, ch ⁇ ⁇ e ⁇ vaya ⁇ ⁇ du ⁇ e ⁇ emescheniya mixture ⁇ ame ⁇ a ⁇ e ⁇ m ⁇ dinamiches ⁇ g ⁇ vy ⁇ avnivaniya vy ⁇ lnena as di ⁇ uz ⁇ a with ⁇ is ⁇ y ⁇ vann ⁇ y tsilind ⁇ iches ⁇ y ⁇ ame ⁇ y and v ⁇ aya - as labi ⁇ in ⁇ a with ⁇ iv ⁇ ami, ⁇ i e ⁇ m between e ⁇ imi ⁇ ame ⁇ ami m ⁇ zhe ⁇ by ⁇ us ⁇ an ⁇ vlen ⁇ il ⁇ , connected with its own outputs with the source of the return of the original fuel and with the accumulation capacity of the sediment.
  • non-hazardous gases such as lead to gas
  • P ⁇ i e ⁇ m themselves us ⁇ ys ⁇ va yavlyayu ⁇ sya b ⁇ lee ⁇ e ⁇ n ⁇ l ⁇ gichnymi than izves ⁇ nye, imeyu ⁇ b ⁇ lee vys ⁇ uyu nadezhn ⁇ s ⁇ , ⁇ a ⁇ ⁇ a ⁇ ⁇ zv ⁇ lyayu ⁇ ves ⁇ i ⁇ tsess ⁇ i b ⁇ lee May 2 niz ⁇ i ⁇ davleniya ⁇ and ⁇ em ⁇ e ⁇ a ⁇ u ⁇ a ⁇ and in connection with e ⁇ im snizhayu ⁇ sya ⁇ izv ⁇ ds ⁇ vennye za ⁇ a ⁇ y in ⁇ m including ene ⁇ g ⁇ za ⁇ a ⁇ y.
  • FIG. 1 devices for modifying a large fuel are shown.
  • Fuel source in the form of capacity 1 of the original fuel and oil pump 2 is connected to the exhaust gas 3.
  • Generator 4 is connected to the electrical outlet 5
  • the factory is in the capacity of 1 initial fuel, and the second - in the capacity of the 14th of the final product.
  • the original cylindrical chamber 7 and the diffuser 9 are equipped with electromagnet filters 15, which prevent the accumulation of mixture fractions on their walls.
  • the original fuel from the refueling unit is sold to 1 original fuel, where it is heated depending on the type of composition, it is 50 ° C up to 80 ° C and is available to us
  • Diffuser 9 and a cylindrical chamber 10 ensure the production of a single cross section of the emulsion flow with a separate distribution of the leveling
  • thermodynamic parameters When this is done, chemical reactions, electrical disturbances and electrical disturbances occur due to the formation of foam and various hydraulics.
  • the emulsion is supplied in
  • FIG. 2 Another option for modifying hydrocarbon fuel is available in FIG. 2.
  • Chamber 12 is optionally connected to its second outlet with a capacity of 20 discharge sediments and a pipe 21 with capacity 1 of the original product.
  • part of the medium is in a gas or
  • the device operates the following way.
  • Is ⁇ dn ⁇ e ⁇ liv ⁇ zalivayu ⁇ or ⁇ s ⁇ yann ⁇ ⁇ dayu ⁇ sam ⁇ e ⁇ m in em ⁇ s ⁇ 1 is ⁇ dn ⁇ g ⁇ ⁇ liva where eg ⁇ nag ⁇ evayu ⁇ in zavisim ⁇ s ⁇ i ⁇ ⁇ ims ⁇ s ⁇ ava and type ⁇ liva ⁇ 30 50 ° C d ⁇ 80 ° C and ⁇ m ⁇ schyu maslyan ⁇ g ⁇ nas ⁇ sa 2 ⁇ dayu ⁇ a predetermined ⁇ as ⁇ d ⁇ m ⁇ , ⁇ edelyaemym ⁇ ebuem ⁇ y ⁇ izv ⁇ di ⁇ eln ⁇ s ⁇ yu ⁇ g ⁇ v ⁇ mu ⁇ livu ⁇ i na ⁇ e ⁇ on v ⁇ d ezhe ⁇ a 3 ⁇ uda ⁇ dn ⁇ v ⁇ emenn ⁇ vsasyvae ⁇ sya che ⁇ ez ⁇ a
  • the emulsion is supplied to the filter 11 of a large variety of types, where the plant is divided,
  • the enriched fuel is available in the separation chamber 12 and then for activation and the full separation for the electrical operations - in the electrical unit 19.
  • the working capacity of this capacity is unambiguously shared by the required production unit.
  • the electrohydrodynamic separator is selected taking into account the interim return of water up to 25% of the waste of fuel and depletion.
  • the claimed invention will find a wide application for the manufacture of non-continuous, inactive and chemical products, including those used in the automotive industry. 40

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

L'invention relève du domaine de la chimie et concerne notamment une technologie de traitement de carburant hydrocarboné, y compris de carburant pour moteurs. L'invention permet d'obtenir un carburant à indices d'octane et de cétane élevés au moyen du procédé suivant: l'alimentation en carburant initial se fait simultanément avec l'éjection; un gaz contenant de l'ozone est alimenté dans la zone d'éjection; des flux turbulents sont créés par le déplacement du mélange ainsi formé; le mélange transformé est acheminé dans un volume à niveau de pression stable; on effectue ensuite l'égalisation thermodynamique des paramètres du mélange. Lors de l'égalisation thermodynamique, on injecte dans le mélange de l'eau pulvérisée. Le procédé de l'invention est mis en oeuvre au moyen de dispositifs munis d'un éjecteur qui possède un tuyau d'aspiration relié à un générateur d'ozone, une entrée reliée à la source d'alimentation en carburant initial et une sortie reliée à un appareil d'enrichissement et de transformation du carburant, ledit appareil étant constitué de chambres cylindriques à circulation directe reliées en série, entre lesquelles est disposé un convertisseur électrohydrodynamique de flux, et d'une ou de deux chambres d'égalisation thermodynamique. Dans ce dernier cas de figure, le dispositif est muni d'une source d'alimentation en eau pulvérisée et d'un séparateur électrohydrodynamique.
PCT/RU2000/000380 1999-10-20 2000-09-25 Procede de modification de carburant hydrocarbone et dispositifs de modification de carburant hydrocarbone WO2001029153A1 (fr)

Priority Applications (7)

Application Number Priority Date Filing Date Title
CA002386612A CA2386612A1 (fr) 1999-10-20 2000-09-25 Procede de modification de carburant hydrocarbone et dispositifs correspondant
JP2001531940A JP2003512503A (ja) 1999-10-20 2000-09-25 炭化水素燃料を改質する方法及び炭化水素燃料を改質するためのデバイス
EA200200464A EA003680B1 (ru) 1999-10-20 2000-09-25 Способ модификации углеводородного топлива и устройства для его осуществления
AU75643/00A AU7564300A (en) 1999-10-20 2000-09-25 Method for modifying of hydrocarbon fuel and devices for modifying hydrocarbon fuel
US10/110,875 US6692634B1 (en) 1999-10-20 2000-09-25 Method for modifying of hydrocarbon fuel and devices for modifying hydrocarbon fuel
KR1020027004898A KR20020052189A (ko) 1999-10-20 2000-09-25 탄화수소 연료 변환 방법 및 장치
EP00964818A EP1241243A4 (fr) 1999-10-20 2000-09-25 Procede de modification de carburant hydrocarbone et dispositifs de modification de carburant hydrocarbone

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
RU99121719 1999-10-20
RU99121719/04A RU2158748C1 (ru) 1999-10-20 1999-10-20 Способ модификации моторного топлива и устройство для его осуществления

Publications (1)

Publication Number Publication Date
WO2001029153A1 true WO2001029153A1 (fr) 2001-04-26

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PCT/RU2000/000380 WO2001029153A1 (fr) 1999-10-20 2000-09-25 Procede de modification de carburant hydrocarbone et dispositifs de modification de carburant hydrocarbone

Country Status (10)

Country Link
US (1) US6692634B1 (fr)
EP (1) EP1241243A4 (fr)
JP (1) JP2003512503A (fr)
KR (1) KR20020052189A (fr)
CN (1) CN1382200A (fr)
AU (1) AU7564300A (fr)
CA (1) CA2386612A1 (fr)
EA (1) EA003680B1 (fr)
RU (1) RU2158748C1 (fr)
WO (1) WO2001029153A1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008140882A1 (fr) * 2007-05-08 2008-11-20 M-I Llc Traitement en ligne de fluides hydrocarbure avec de l'ozone
US7867376B2 (en) 2004-04-26 2011-01-11 M-I L.L.C. Treatment of hydrocarbon fluids with ozone

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1309806C (zh) * 2005-07-29 2007-04-11 陕西师范大学 提高直馏汽油辛烷值的方法
US7833684B2 (en) 2007-11-14 2010-11-16 Xerox Corporation Toner compositions
WO2012027820A1 (fr) 2010-09-03 2012-03-08 Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Natural Resources Canada Production d'un produit diesel à teneur élevée en cétane
RU2443753C1 (ru) * 2010-12-28 2012-02-27 Общество с ограниченной ответственностью "ЭнергоСтройИнвест" Способ очистки жидких углеводородов
US9488085B2 (en) 2013-09-18 2016-11-08 Advanced Technology Emission Solutions Inc. Catalytic converter structures with induction heating
DE102012109842B4 (de) * 2012-10-16 2023-06-29 Dr. Ing. H.C. F. Porsche Ag Verfahren zum Bestimmen einer Pufferwirkung eines Aktivkohlefilters
US10590819B2 (en) 2013-09-18 2020-03-17 Advanced Technology Emission Solutions Inc. Emission control system with resonant frequency measurement and methods for use therewith
US10590818B2 (en) 2016-11-24 2020-03-17 Advanced Technology Emission Solutions Inc. Emission control system with frequency controlled induction heating and methods for use therewith
US10450915B2 (en) 2013-09-18 2019-10-22 Advanced Technology Emission Solutions Inc. Emission control system with induction heating and methods for use therewith
US10557392B2 (en) 2013-09-18 2020-02-11 Advanced Technology Emission Solutions Inc. Emission control system with temperature measurement and methods for use therewith
KR101676372B1 (ko) 2014-11-25 2016-11-16 (주)에이티엘 회전형 리니어 모터 장치
JP6639341B2 (ja) * 2016-07-14 2020-02-05 ヤンマー株式会社 内燃機関の制御装置および内燃機関の制御方法
CN107541304A (zh) * 2017-08-28 2018-01-05 柳玉庭 一种新型燃气的制备方法

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DE3151614A1 (de) * 1980-12-31 1982-08-26 Chevron Research Co., 94105 San Francisco, Calif. Verfahren zur qualitaetsverbesserung eines kohlenwasserstoffhaltigen oels
JPS58180593A (ja) * 1982-04-16 1983-10-22 Mitsuyoshi Matsuoka 燃料油の改質方法および装置
RU95107109A (ru) * 1995-05-10 1996-06-20 Ю.Н. Просвирнин Способ повышения эффективности работы двигателя внутреннего сгорания и устройство для его осуществления
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WO1998047982A1 (fr) * 1997-04-17 1998-10-29 Marc Jean Campagna Combustible et procede de production de combustible
RU2126094C1 (ru) * 1995-12-01 1999-02-10 Валерий Дмитриевич Дудышев Способ интенсификации работы двигателя внутреннего сгорания

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US4334889A (en) * 1978-01-09 1982-06-15 Toshiaki Takabayashi Method for improving combustibility of liquid fuel
DE3151614A1 (de) * 1980-12-31 1982-08-26 Chevron Research Co., 94105 San Francisco, Calif. Verfahren zur qualitaetsverbesserung eines kohlenwasserstoffhaltigen oels
JPS58180593A (ja) * 1982-04-16 1983-10-22 Mitsuyoshi Matsuoka 燃料油の改質方法および装置
RU2078977C1 (ru) * 1994-02-08 1997-05-10 Евгений Леонидович Блинков Устройство для обработки воздуха в двигателе внутреннего сгорания
RU95107109A (ru) * 1995-05-10 1996-06-20 Ю.Н. Просвирнин Способ повышения эффективности работы двигателя внутреннего сгорания и устройство для его осуществления
RU2126094C1 (ru) * 1995-12-01 1999-02-10 Валерий Дмитриевич Дудышев Способ интенсификации работы двигателя внутреннего сгорания
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7867376B2 (en) 2004-04-26 2011-01-11 M-I L.L.C. Treatment of hydrocarbon fluids with ozone
US8728281B2 (en) 2004-04-26 2014-05-20 M-I L.L.C. Treatment of hydrocarbon fluids with ozone
WO2008140882A1 (fr) * 2007-05-08 2008-11-20 M-I Llc Traitement en ligne de fluides hydrocarbure avec de l'ozone
EA015547B1 (ru) * 2007-05-08 2011-08-30 Эм-Ай ЭлЭлСи Система и способ для поточной обработки озоном углеводородных жидкостей
US8066851B2 (en) 2007-05-08 2011-11-29 M-I L.L.C. In-line treatment of hydrocarbon fluids with ozone
US8882969B2 (en) 2007-05-08 2014-11-11 M-I Llc In-line treatment of hydrocarbon fluids with ozone

Also Published As

Publication number Publication date
EP1241243A4 (fr) 2006-10-18
US6692634B1 (en) 2004-02-17
CN1382200A (zh) 2002-11-27
AU7564300A (en) 2001-04-30
JP2003512503A (ja) 2003-04-02
EA003680B1 (ru) 2003-08-28
RU2158748C1 (ru) 2000-11-10
EA200200464A1 (ru) 2003-02-27
EP1241243A1 (fr) 2002-09-18
KR20020052189A (ko) 2002-07-02
CA2386612A1 (fr) 2001-04-26

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